EP0618835A1 - Filter zur reinigung von gasen. - Google Patents

Filter zur reinigung von gasen.

Info

Publication number
EP0618835A1
EP0618835A1 EP92923902A EP92923902A EP0618835A1 EP 0618835 A1 EP0618835 A1 EP 0618835A1 EP 92923902 A EP92923902 A EP 92923902A EP 92923902 A EP92923902 A EP 92923902A EP 0618835 A1 EP0618835 A1 EP 0618835A1
Authority
EP
European Patent Office
Prior art keywords
filter
layer
coalescing
end cap
drainage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP92923902A
Other languages
English (en)
French (fr)
Other versions
EP0618835B1 (de
Inventor
Alex George Hunter
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
PSI Global Ltd
Original Assignee
Process Scientific Innovations Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Process Scientific Innovations Ltd filed Critical Process Scientific Innovations Ltd
Publication of EP0618835A1 publication Critical patent/EP0618835A1/de
Application granted granted Critical
Publication of EP0618835B1 publication Critical patent/EP0618835B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2411Filter cartridges
    • B01D46/2414End caps including additional functions or special forms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/003Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions including coalescing means for the separation of liquid
    • B01D46/0031Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions including coalescing means for the separation of liquid with collecting, draining means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/52Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material
    • B01D46/521Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material using folded, pleated material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2275/00Filter media structures for filters specially adapted for separating dispersed particles from gases or vapours
    • B01D2275/10Multiple layers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2275/00Filter media structures for filters specially adapted for separating dispersed particles from gases or vapours
    • B01D2275/30Porosity of filtering material

Definitions

  • the present invention relates to a filter for gas and to its use for the filtration of a stream of gas contaminated with liquid in the form of mist.
  • the filter is generally tubular and comprises a coalescing layer 10 of microporous material which fits closely between inner and outer fora inous metal cylinders 12,14 and extends between upper and lower end caps 16,18.
  • the upper end cap 16 is formed with a port 20 to permit the stream 22 of oil-contaminated air to enter the interior of ⁇ the filter and the lo .er end cap 18 is closed as shown.
  • the coalescing layer 10 is sealed gas-tightly to the end caps 16,18 by a curable sealant 20, e.g.
  • the coalescing layer 10 is in this instance of one or more pleated sheets of resin-impregnated borosilicate glass microfibres as disclosed in Patent No. GB-A-1557821.
  • An alternative form of coalescing layer which is formed by moulding is disclosed in Patent No. GB-A-1603519.
  • a drainage layer 24 which in this instance is of an open-celled foam plastics material, although coalescing filters whose drainage layers are of a felted fabric material e.g. , as disclosed in our Patent Specification No. PCT/GB 89/00182 are also known.
  • the drainage layer is preferably treated with a fluorocarbon.
  • the air entering the filter travels radially outward through the coalescing layer 10 and through the drainage layer 24 from which it is discharged radially as indicated at 26.
  • Coalescing filters of this kind can be used in a number of attitudes, but this invention is concerned with coalescing filters which are intended to depend vertically downwards from a filter head and to fit with the removable bowl of such a filter head.
  • Droplets of oil carried with the air 22 are coalesced by the microporous coalescing layer 22 where the individual tiny droplets are combined, and the oil is carried outwards to the drainage layer 24 where it - 3 - flows downwards to form an oil-saturated band or wet zone 28 at the lower end of the drainage layer 24, the oil gradually dropping from the wet zone 24 as individual large drops 30.
  • the wet zone 28 which forms in normal use of the filter is of sufficient height that a significant portion thereof is in overlapping relationship with the coalescing layer 10. Air from the lower part of the coalescing filter 10 is forced to travel outward through the wet zone 28 where it disturbs the oil and can form bursting bubbles on or adjacent the outer surface of the drainage layer 24. These bursting bubbles of oil in the wet zone 28 re-form fine oil particles on the clean side of the filter which are carried into the clean air stream 26 and reduce the filtration efficiency.
  • coalescing filter shown in Figure 1 is unusual in that the lower end of the drainage layer 24 is not confined within the lower end cap 18 but is free on th- outsi e thereof. More usually, both the coalescing and the drainage layer fit on or into the lower end cap as is shown in Patent No. GB-A-1345155.
  • the filter may be connected to the filter head with which it is intended to be used by a screw connection 32 in the top cap 16.
  • a tie rod threaded at its lower end can depend from the filter head and can fit into a threaded socket in the end cap 18.
  • the filter may also fit to the filter head by a bayonet connection. With all these arrangements, during the fitting operation the filter is gripped in the fingers of, the user's hand at its lower end and is offered up to the filter head where it is twisted or screwed into position.
  • This invention is based on the realisation that provided the drainage layer is undisturbed at its lower end and terminates at a quiet region axially below the coalescing layer, the oil saturated band or wet zone that forms in the drainage layer can be caused substantially not to overlap the coalescing layer or do so to a greatly reduced extent.
  • the disturbance which can lead to an undesired increase in the height of the wet zone includes pressure, compression or indenting of the drainage layer, for example when it is pressed into a channel in an end cap and also includes compression of the lower end of the drainage layer 24 by handling with the user's fingers when the filter is fitted to the filter head.
  • Disturbance which raises the height of the wet band also includes obstructing the lower end of the drainage layer so that the initial escape of oil therefrom is solely through the side and not through the end of the drainage layer.
  • the invention provides a tubular filter for fitting into a housing with, its axis vertical and for filtration of a stream of gas contaminated with liquid in the form of mist, the filter comprising a microporous filter layer for coalescing the mist as the gas flows through the filter, a macroporous drainage layer into which coalesced liquid flows from the filter layer and then runs to a lower end o. the filter layer from which it drains as droplets, and an end cap which fits gas-tightly to the filter layer to close the lower end of the filter, characterised in that it has one or more of the following features:
  • the drainage layer extends below the filter layer; - 6 - (b) the drainage layer extends axially into the end cap, there being drainage channels through the base of the end cap;
  • the end cap is formed to provide a dual purpose guard which surrounds the lower extremity of the drainage layer, and acts as a finger grip to permit mounting of the filter cartridge to the filter head without cqntact with the drainage layer.
  • the invention also provides the use for the filtration of a stream of gas contaminated with liquid in the form of mist of a tubular filter through which the gas passes, the filter being supported from a head of a filter housing so as to depend from the head with its axis vertical, and the filter comprising a microporous filter layer for coalescing the mist as the gas flows through the filter, a macroporous drainage layer into which coalesced liquid from the filter layer flows from the filter layer and then runs to the lower end of the filter from which it drains as drops, and an end cap which fits gas-tightly to the filter layer to close the lower end of the filter with the drainage layer having an undisturbed lower end that terminates at a quiet zone axially below the filter layer to achieve the effect that the height of an oil saturated band at the lowest region of the drainage layer is reduced.
  • Figure 1 is a perspective view of a prior art coalescing filter
  • Figure 2 is a half-sectioned elevation of a filter according to the invention.
  • Figure 3 is a perspective view of a lower end cap forming part of the filter of Figure 2;
  • Figure 4 is a perspective view of an alternative form of the end cap.
  • FIG 2 there is shown a coalescing filter of similar overall construction to tnat of Figure 1, except that the top end cap 16a no longer has a threaded connection and the lower end cap 18a which, is moulded in glass-filled nylon or other suitable plastic material has on its inner end an internally threaded boss 40 which fits onto a threaded lower end 42 of a tie rod 44 depending from a filter head (not shown) .
  • An upwardly facing flange 46 defines with the boss 44 and the intervening portions of the end cap 18a a channel into which the inner and outer foraminous cylinders 12,14, and the coalescing layer 10 are secured by resin 48.
  • a plurality of relatively thin widely-spaced radial ribs 50 support an annular guard 52 in spaced relationship surrounding the lower end of the drainage layer 24 which rests on the ribs 50 but is otherwise unobstructed.
  • the relatively large slots 51 which are defined between adjacent pairs of ribs 50 allow generally unobstructed drainage of droplets from the drainage layer 24.
  • the guard 52 defines a relatively quiet zone for formation of the oil droplets i.e. air flow around the wet band is minimised.
  • Finger grips 54 on the outside of the guard 52 enable the filter element to be tightened onto the end cap without risk of damage to the drainage layer.
  • the end cap construction of Figure 4 is generally similar to that of Figure 3 except that the continuous guard 52 is replaced by a multiplicity of angularly spaced fingers 60, such that the drainage layer 24 fits between the fingers 60 and the flange 46.
  • a filter according to the invention can provide a significant reduction in pressure drop at igh flow rates of air, that the amount of oil mist appearing on the clean si e of the filter is more than twice the amount of oil mist present using a coalescing filter of otherwise similar construction, except that the drainage sleeve is tightly fitted into a channel in the end cap.
  • the oil drainage layer used is typically a PVC impregnated reticulated polyether or polyurethane foam having typically 60 pores per inch and optionally impregnated with a luorocarbon.
  • the drainage layer can also be a felt of polyester or other material which may be impregnated with a fluorocarbon.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Geometry (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Filtering Materials (AREA)
  • Glass Compositions (AREA)
EP92923902A 1991-11-26 1992-11-24 Filter zur reinigung von gasen Expired - Lifetime EP0618835B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB9125140A GB2261830B (en) 1991-11-26 1991-11-26 Filter for purification of gas
GB9125140 1991-11-26
PCT/GB1992/002167 WO1993010881A1 (en) 1991-11-26 1992-11-24 Filter for purification of gas

Publications (2)

Publication Number Publication Date
EP0618835A1 true EP0618835A1 (de) 1994-10-12
EP0618835B1 EP0618835B1 (de) 1995-10-11

Family

ID=10705274

Family Applications (1)

Application Number Title Priority Date Filing Date
EP92923902A Expired - Lifetime EP0618835B1 (de) 1991-11-26 1992-11-24 Filter zur reinigung von gasen

Country Status (8)

Country Link
EP (1) EP0618835B1 (de)
JP (1) JPH07501479A (de)
AT (1) ATE128884T1 (de)
DE (1) DE69205440T2 (de)
DK (1) DK0618835T3 (de)
ES (1) ES2079900T3 (de)
GB (1) GB2261830B (de)
WO (1) WO1993010881A1 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017174199A1 (en) * 2016-04-07 2017-10-12 Donaldson Filtration Deutschland Gmbh Filter element for filtering a fluid passing through the filter element, coalescence filter, compressed air filter system, use of a filter element and a method of producing a coalescence filter

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2295970A (en) * 1994-12-16 1996-06-19 Process Scient Innovations Filter assembly and cartridge therefor
US5803941A (en) * 1995-01-12 1998-09-08 Donaldson Company, Inc. Filter element
JP3722492B2 (ja) * 1995-01-12 2005-11-30 ドナルドソン・カンパニー・インコーポレーテッド フィルタ要素
DE19508815A1 (de) * 1995-03-11 1996-09-12 Mann & Hummel Filter Luftentölelement
GB2300367A (en) * 1995-05-04 1996-11-06 Process Scient Innovations Conductive filter
US5961678A (en) * 1995-07-07 1999-10-05 Flair Corporation Filter drainage layer attachment
JP2000508581A (ja) * 1996-04-17 2000-07-11 ポール・コーポレーション 使い捨てコアレッサー
AU1675099A (en) 1997-12-15 1999-07-05 Domnick Hunter Limited Filter assembly
US6663685B2 (en) 1997-12-15 2003-12-16 Domnick Hunter Limited Filter assembly
US6391197B1 (en) 1997-12-15 2002-05-21 Domnick Hunter Limited Filter assembly
DE69824631T2 (de) 1997-12-15 2005-06-23 Domnick Hunter Limited Filteranlage
WO1999030798A1 (en) * 1997-12-15 1999-06-24 Domnick Hunter Limited Filter assembly
US6416563B1 (en) 1997-12-15 2002-07-09 Domnick Hunter Limited Filter assembly
GB2335867A (en) * 1998-04-03 1999-10-06 Process Scient Innovations Thermally bonded felt material for coalescence filters
DE19827297A1 (de) * 1998-06-19 1999-12-23 Mann & Hummel Filter Vorrichtung zur Abscheidung einer Phase aus einem zu reinigenden Fluid
GB0417459D0 (en) 2004-08-05 2004-09-08 Domnick Hunter Ltd Filter assembly
GB0417455D0 (en) * 2004-08-05 2004-09-08 Domnick Hunter Ltd Filter element
US8057567B2 (en) 2004-11-05 2011-11-15 Donaldson Company, Inc. Filter medium and breather filter structure
KR101514908B1 (ko) 2004-11-05 2015-04-23 도날드슨 컴파니, 인코포레이티드 필터 매체 및 구조
US7686859B2 (en) 2005-08-04 2010-03-30 Johnson Controls Technology Company Coalescing filter element with drainage mechanism
ATE495811T1 (de) 2005-08-16 2011-02-15 Donaldson Co Inc Luftreiniger mit verdrehsicherer anordnung und verfahren
US7416576B2 (en) * 2006-01-27 2008-08-26 Mecs, Inc. Fiber bed assembly and fiber bed therefor
GB2448865B (en) 2007-04-16 2011-10-26 Psi Global Ltd Improvements in coalescing filters
US8361181B2 (en) 2008-06-06 2013-01-29 Donaldson Company, Inc. Air cleaner assemblies; filter cartridges therefor; features; and, methods
AT512190B1 (de) * 2012-01-27 2013-06-15 Ift Gmbh Vorrichtung zur abscheidung von stoffen
US9144760B2 (en) 2012-07-03 2015-09-29 The University Of Akron Liquid drainage from coalescing filter medium with drainage channels
AT512506B1 (de) * 2012-08-24 2013-09-15 Ift Gmbh Filtereinrichtung
ITPD20130091A1 (it) * 2013-04-10 2014-10-11 Ocs Cold S R L Separatore olio con elemento integrato denominato elemento separatore olio retex inverter formato da un tubo con taglio o fori, lana metallica, rete metallica
DE102014003486A1 (de) * 2014-03-14 2015-09-17 Berner International Gmbh Filterpatrone für eine Sicherheitswerkbank und Sicherheitswerkbank mit mindestens einer Filterpatrone
JP6519862B2 (ja) * 2015-05-11 2019-05-29 Smc株式会社 空気圧フィルタ及びフィルタエレメント
US9908070B2 (en) 2015-11-23 2018-03-06 Pall Corporation Fuel tank inerting prefilter assemblies, devices, and methods of use
JP6647553B2 (ja) * 2016-03-01 2020-02-14 Smc株式会社 フィルタエレメント
BE1025322B1 (nl) 2017-06-12 2019-01-29 Atlas Copco Airpower Naamloze Vennootschap Coalescentiefilter
GB2583692A (en) 2019-02-28 2020-11-11 Psi Global Ltd Filter cartridge and casing
BR112021018538A2 (pt) * 2019-03-20 2021-11-23 Smc Corp Elemento de filtro
GB202003117D0 (en) 2020-03-04 2020-04-15 Parker Hannifin Emea Sarl Filter element assembly
US20210394094A1 (en) * 2020-06-23 2021-12-23 Pall Corporation Filter arrangement including prefiltration filter element and filter device

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1236396A (en) * 1967-08-17 1971-06-23 Norgren Ltd C A Apparatus for the filtration of air or other gaseous media
DE2510225C2 (de) * 1974-03-11 1986-09-11 Pall Corp., Glen Cove, N.Y. Vorrichtung zum Abscheiden von in Gasen schwebenden Flüssigkeiten
GB1479753A (en) * 1974-06-20 1977-07-13 Norgren Ltd C Apparatus for the filtration of air of other gaseous medi
US4053290A (en) * 1976-10-18 1977-10-11 Monsanto Company Fiber bed separator
US4231768A (en) * 1978-09-29 1980-11-04 Pall Corporation Air purification system and process
GB2033247B (en) * 1978-10-18 1982-11-03 Process Scient Innovations Filter silencer for compressed gas stream
JPS5676017U (de) * 1979-11-13 1981-06-20
GB2126497A (en) * 1982-09-09 1984-03-28 Domnick Hunter Filters Ltd Coalescing filter element
EP0139639A1 (de) * 1983-03-16 1985-05-08 Whatman Reeve Angel Plc Filterpatrone mit endkappe
GB8703314D0 (en) * 1987-02-13 1987-03-18 Process Scient Innovations Air/oil separator
GB2222534B (en) * 1988-09-09 1992-11-25 Process Scient Innovations Filter assembly and cartridge therefor

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9310881A1 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017174199A1 (en) * 2016-04-07 2017-10-12 Donaldson Filtration Deutschland Gmbh Filter element for filtering a fluid passing through the filter element, coalescence filter, compressed air filter system, use of a filter element and a method of producing a coalescence filter
US10940405B2 (en) 2016-04-07 2021-03-09 Donaldson Filtration Deutschland Gmbh Filter element for filtering a fluid passing through the filter element, coalescence filter, compressed air filter system, use of filter element and a method of producing a coalescence filter

Also Published As

Publication number Publication date
DE69205440T2 (de) 1996-05-15
GB2261830A (en) 1993-06-02
GB9125140D0 (en) 1992-01-22
DE69205440D1 (de) 1995-11-16
WO1993010881A1 (en) 1993-06-10
JPH07501479A (ja) 1995-02-16
ES2079900T3 (es) 1996-01-16
ATE128884T1 (de) 1995-10-15
EP0618835B1 (de) 1995-10-11
DK0618835T3 (da) 1995-12-04
GB2261830B (en) 1995-07-26

Similar Documents

Publication Publication Date Title
EP0618835B1 (de) Filter zur reinigung von gasen
EP1059994B1 (de) Konisch geformter luft/öl-trenner
US5961678A (en) Filter drainage layer attachment
US5545315A (en) Water filtering and purifying apparatus
KR101538182B1 (ko) 필터 조립체 및 필터 조립체를 통한 유동 지향 방법
EP0601196B1 (de) Filtersystem für druckluft
CA1337474C (en) Method for gas-liquid separation and filtration
GB2033247A (en) Filter Silencer for Compressed Gas Stream
EP3458174B1 (de) Filteranordnung und verfahren zur filtrierung
WO1995005234B1 (en) Mist collector cartridge
EP3930872B1 (de) Filterpatrone und gehäuse
CN109011912B (zh) 聚结过滤器
GB2295970A (en) Filter assembly and cartridge therefor
CN113828048A (zh) 包括预过滤过滤元件的过滤器组件和过滤器装置
EP1839728B1 (de) Lufttrocknerpatrone
KR102353343B1 (ko) 공기 청정 장치
EP1181969A1 (de) Verfahren und Vorrichtung zur Abscheidung von Schwefelsäurenebel aus Gasen
KR102412475B1 (ko) 집진 장치
US5030262A (en) Air vapor trap and drain therefore
GB2251812A (en) Oil-water separator
WO2020188800A1 (ja) フィルタエレメント
RU4241U1 (ru) Влагоотделитель

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19940624

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR IT LI NL SE

17Q First examination report despatched

Effective date: 19941214

RBV Designated contracting states (corrected)

Designated state(s): AT BE CH DE DK ES FR IT LI NL SE

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE DK ES FR IT LI NL SE

REF Corresponds to:

Ref document number: 128884

Country of ref document: AT

Date of ref document: 19951015

Kind code of ref document: T

ET Fr: translation filed
REF Corresponds to:

Ref document number: 69205440

Country of ref document: DE

Date of ref document: 19951116

ITF It: translation for a ep patent filed

Owner name: ING. ZINI MARANESI & C. S.R.L.

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2079900

Country of ref document: ES

Kind code of ref document: T3

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19981109

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19981111

Year of fee payment: 7

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991124

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991130

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991130

REG Reference to a national code

Ref country code: FR

Ref legal event code: CD

NLT1 Nl: modifications of names registered in virtue of documents presented to the patent office pursuant to art. 16 a, paragraph 1

Owner name: PSI GLOBAL LTD

REG Reference to a national code

Ref country code: ES

Ref legal event code: PC2A

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20001006

Year of fee payment: 9

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20001025

Year of fee payment: 9

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DK

Payment date: 20001107

Year of fee payment: 9

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20011124

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20011125

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20011125

EUG Se: european patent has lapsed

Ref document number: 92923902.8

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20021213

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20081120

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20081215

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20081128

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20090123

Year of fee payment: 17

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20081124

BERE Be: lapsed

Owner name: *PSI GLOBAL LTD

Effective date: 20091130

REG Reference to a national code

Ref country code: NL

Ref legal event code: V1

Effective date: 20100601

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20100730

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20100601

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091130

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20100601

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20081127

Year of fee payment: 17

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091124